Viscoelastic surfactant fluids and related methods of use

ABSTRACT

Viscoelastic surfactant based aqueous fluid systems useful as thickening agents in various applications, e.g. to suspend particles produced during the excavation of geologic formations. The surfactants are zwitterionic/amphoteric surfactants such as dihydroxyl alkyl glycinate, alkyl ampho acetate or propionate, alkyl betaine, alkyl amidopropyl betaine and alkylimino mono- or di-propionates derived from certain waxes, fats and oils. The thickening agent is used in conjunction with an inorganic water-soluble salt or organic additive such as phthalic acid, salicylic acid or their salts.

This application is a continuation application of U.S. Ser. No.09/093,131, filed Jun. 8, 1998, which claims the benefit of thedisclosure of U.S. Provisional Patent Application Ser. Nos. 60/049,045,filed on Jun. 10, 1997, and 60/054,455, filed on Aug. 5, 1997. Thedisclosure of U.S. Ser. No. 09/093,131, filed Jun. 8, 1998, isincorporated herein it its entirety.

FIELD OF THE INVENTION

This invention relates to viscoelastic fluids which contain a surfactantand to methods of suspending particles using such viscoelastic fluids.

BACKGROUND OF THE INVENTION

It is known to thicken the aqueous phase of a suspension of solidparticles or emulsified droplets. The addition of thickeners increasesthe viscosity of the aqueous phase and thereby retards settling of theparticles or droplets. Such retardation is useful to maintain theparticles or droplets in suspension during the storage, use, and/ortransport of the suspension

Polymeric thickeners, e.g. starches, which thicken by entanglement ofthe polymeric chains, have been used to viscosify the aqueous phase ofsuspensions. Such thickeners can degrade under the influence ofmechanical shear or chemical scission (e.g. by oxidation or hydrolysis)of the polymeric chains which results in a loss of viscosity and, thus,suspension stability.

Cationic surfactants have been found which form rod-like micelles undercertain conditions. The presence of the rod-like micelles imparts to thefluid viscoelastic properties. However, cationic surfactants tend tohave high toxicity and very low biodegradability.

SUMMARY OF THE INVENTION

The present invention provides a viscoelastic fluid useful as athickener for the suspension of particles. The viscoelastic fluidsconsist of an amphoteric/zwitterionic surfactant and an organicacid/salt and/or inorganic salts.

Thus, this invention specifically relates to a viscoelastic fluidcomprising:

(1) an aqueous medium;

(2) an amount of a surfactant selected from the group consisting ofamphoteric surfactants, zwitterionic surfactants, and mixtures thereof,effective to render said aqueous medium viscoelastic; and

(3) a member selected from the group consisting of organic acids,organic acid salts, inorganic salts, and combinations of one or moreorganic acids or organic acid salts with one or more inorganic salts.

In yet another embodiment of the present invention, the inventionrelates to a viscoelastic fluid consisting essentially of:

(1) an aqueous medium;

(2) an amount of a surfactant comprising an amine oxide surfactant; and

(3) an anionic surfactant containing a hydrophobe having at least 14carbon atoms.

The term “viscoelastic” refers to those viscous fluids having elasticproperties, i.e., the liquid at least partially returns to its originalform when an applied stress is released. The thickened aqueousviscoelastic fluids are useful as water-based hydraulic fluids inlubricant and hydraulic fracturing fluids to increase permeability inoil production.

The present invention also relates to a method for distributingsuspended solid particles such as excavation by-products in a fluidcomprised of the viscoelastic fluid of this invention, wherein the solidparticles remain suspended for an extended period of time to a side, bytransporting the fluid to a site while the solid particles remainsuspended in the fluid and depositing the fluid to such site.

This invention also relates to a method for fracturing a subterraneanformation comprising pumping the inventive viscoelastic fluid through awellbore and into a subterranean formation at a pressure sufficient tofracture the formation.

This invention also relates to a detergent formulation comprising adetersive surfactant in admixture with a viscoelastic fluid of thisinvention.

This invention also relates to the use of the viscoelastic fluid as adrift control agent for agricultural formulations. In this regard, thisinvention relates to an aqueous formulation of an agricultural chemicaland an amount of the viscoelastic fluid of this invention sufficient toincrease the average droplet size of a spray of said formulation.

BRIEF DESCRIPTION OF THE FIGURES

FIG. 1 shows viscosity versus shear rate for a viscoelastic surfactantsolution prepared by adding 5 percent of disodiumtallowiminodipropionate (Mirataine T2C®) and 2.25 percent of phthalicacid to water.

FIG. 2 shows the dynamic modulus G′(storage modulus) and G″ (lossmodulus) at 25° C. and 50° C. of the same solution as FIG. 1.

FIG. 3 shows the viscosity versus shear rate for a viscoelasticsurfactant solution prepared by adding 5 percent of disodiumtallowiminodipropionate (Mirataine T2C®), 4 percent of NH₄Cl and 1.75˜2.0 percent of phthalic acid to water.

FIG. 4 shows the viscosity versus shear rate for viscoelastic surfactantsolutions prepared by adding 4 or 5 percent of disodium oleamidopropylbetaine (Mirataine BET-O®), 3 percent of KCl and 0.5 percent of phthalicacid to water.

FIG. 5 shows the dynamic modulus G′ (storage modulus) and G″ (lossmodulus) at 25° C. and 50° C. of the same solution as FIG. 4.

DETAILED DESCRIPTION OF THE INVENTION

The property of viscoelasticity in general is well known and referenceis made to S. Gravsholt, Journal of Coll. And Interface Sci., 57(3), 575(1976); Hoffmann et al., “Influence of Ionic Surfactants on theViscoelastic Properties of Zwitterionic Surfactant Solutions”, Langmuir,8, 2140-2146 (1992); and Hoffmann et al., The Rheological Behaviour ofDifferent Viscoelastic Surfactant Solutions, Tenside Surf. Det., 31,389-400, 1994. Of the test methods specified by these references todetermine whether a liquid possesses viscoelastic properties, one testwhich has been found to be useful in determining the viscoelasticity ofan aqueous solution consists of swirling the solution and visuallyobserving whether the bubbles created by the swirling recoil after theswirling is stopped. Any recoil of the bubbles indicatesviscoelasticity. Another useful test is to measure the storage modulus(G′) and the loss modulus (G″) at a given temperature. If G′>G″ at somepoint or over some range of points below about 10 rad/sec, typicallybetween about 0.001 to about 10 rad/sec, more typically between about0.1 and about 10 rad/sec, at a given temperature and if G′>10⁻² Pascals,preferably 10⁻¹ Pascals, the fluid is typically considered viscoelasticat that temperature. Rheological measurements such as G′ and G″ arediscussed more fully in “Rheological Measurements”, Encyclopedia ofChemical Technology, vol. 21, pp. 347-372, (John Wiley & Sons, Inc.,N.Y., N.Y., 1997, 4th ed.). To the extent necessary for completion, theabove disclosures are expressly incorporated herein by reference.

Viscoelasticity is caused by a different type of micelle formation thanthe usual spherical micelles formed by most surfactants. Viscoelasticsurfactant fluids form worm-like, rod-like or cylindrical micelles insolution. The formation of long, cylindrical micelles creates usefulrheological properties. The viscoelastic surfactant solution exhibitsshear thinning behavior, and remains stable despite repeated high shearapplications. By comparison, the typical polymeric thickener willirreversibly degrade when subjected to high shear.

In the summary of the invention and this detailed description, eachnumerical value should be read once as modified by the term “about”(unless already expressly so modified), and then read again as not somodified, unless otherwise indicated in context.

The viscoelastic surfactants can be either ionic or nonionic. Thepresent invention comprises an aqueous viscoelastic surfactant based onamphoteric or zwitterionic surfactants. The amphoteric surfactant is aclass of surfactant that has both a positively charged moiety and anegatively charged moiety over a certain pH range (e.g. typicallyslightly acidic), only a negatively charged moiety over a certain pHrange (e.g. typically slightly alkaline) and only a positively chargedmoiety at a different pH range (e.g. typically moderately acidic), whilea zwitterionic surfactant has a permanently positively charged moiety inthe molecule regardless of pH and a negatively charged moiety atalkaline pH.

The viscoelastic fluid comprises water, surfactant, and a water-solublecompound selected from the group consisting of organic acids, organicacid salts, inorganic salts, and mixtures thereof. Alternatively, theviscoelastic fluid can comprise water, an amine oxide surfactant and ananionic surfactant containing a hydrophobe having at least about 14carbon atoms. The viscoelastic surfactant solution is useful as afracturing fluid or water-based hydraulic fluid. The viscoelastic fluidused as a fracturing fluid may optionally contain a gas such as air,nitrogen or carbon dioxide to provide an energized fluid or a foam.

The component of the fluid which will be present in the greatestconcentration is water, i.e. typically water will be a major amount byweight of the viscoelastic fluid. Water is typically present in anamount by weight greater than or equal to about 50% by weight of thefluid. The water can be from any source so long as the source containsno contaminants which are incompatible with the other components of theviscoelastic fluid (e.g., by causing undesirable precipitation). Thus,the water need not be potable and may be brackish or contain othermaterials typical of sources of water found in or near oil fields.

Examples of zwitterionic surfactants useful in the present invention arerepresented by the formula:

wherein R₁ represents a hydrophobic moiety of alkyl, alkylarylalkyl,alkoxyalkyl, alkylaminoalkyl and alkylamidoalkyl, wherein alkylrepresents a group that contains from about 12 to about 24 carbon atomswhich may be branched or straight chained and which may be saturated orunsaturated. Representative long chain alkyl groups include tetradecyl(myristyl), hexadecyl (cetyl), octadecentyl (oleyl), octadecyl(stearyl), docosenoic (erucyl) and the derivatives of tallow, coco, soyaand rapeseed oils. The preferred alkyl and alkenyl groups are alkyl andalkenyl groups having from about 16 to about 22 carbon atoms.Representative of alkylamidoalkyl is alkylamidopropyl with alkyl beingas described above.

R₂ and R₃ are independently an aliphatic chain (i.e. as opposed toaromatic at the atom bonded to the quaternary nitrogen, e.g., alkyl,alkenyl, arylalkyl, hydroxyalkyl, carboxyalkyl, andhydroxyalkyl-polyoxyalkylene, e.g. hydroxyethyl-polyoxyethylene orhydroxypropyl-polyoxypropylene) having from 1 to about 30 atoms,preferably from about 1 to about 20 atoms, more preferably from about 1to about 10 atoms and most preferably from about 1 to about 6 atoms inwhich the aliphatic group can be branched or straight chained, saturatedor unsaturated. Preferred alkyl chains are methyl, ethyl, preferredarylalkyl is benzyl, and preferred hydroxyalkyls are hydroxyethyl orhydroxypropyl, while preferred carboxyalkyls are acetate and propionate.

R₄ is a hydrocarbyl radical (e.g. alkylene) with chain length 1 to 4.Preferred are methylene or ethylene groups.

Specific examples of zwitterionic surfactants include the followingstructures:

wherein R₁ has been previously defined herein.

Examples of amphoteric surfactants include those represented by formulaVI:

wherein R₁, R₂, and R₄ are the same as defined above.

Other specific examples of amphoteric surfactants include the followingstructures:

wherein R₁ has been previously defined herein, and X is an inorganiccation such as Na⁺, K⁺, NH₄ ⁺ associated with a carboxylate group orhydrogen atom in an acidic medium.

A typical chemical process to synthesize dihydroxy ethoxylate glycinatestarting from ethoxylated alkylamine is as follows:

The final products may also include some unreacted starting dihydroxyethyl alkyl amine, and small amounts of sodium glycolate, diglycolateand sodium chloride as by products. A similar process can be used toprepare propoxylated analogues.

A typical chemical process to synthesize alkyliminiodipropionate fromalkyl amine is as follows:

The final products will also include a small amount of methanol,unreacted acrylic acid, alkylamine and some oligomeric acrylate or acidas by products.

A typical chemical process to synthesize alkylamidopropyl betaine fromalkyl amine is as follows:

The final products will also include a small amount of sodium glycolate,diglycolate, sodium chloride and glycerine as by products.

In still another embodiment of the invention, the zwitterionicsurfactant selected is an amine oxide. This material has the followingstructure:

where R₁, R₂ and R₃ are as defined above.

The surfactants are used in an amount which in combination with theother ingredients is sufficient to form a viscoelastic fluid, whichamount will typically be a minor amount by weight of the fluid (e.g.less than about 50% by weight). The concentration of surfactant canrange from about 0.5% to about 10% percent by weight of the fluid, moretypically from about 0.5% to about 8%, and even more typically fromabout 0.5% to about 6%. Optimum concentrations for any particular set ofparameters can be determined experimentally.

The fluid also comprises one or more members from the group of organicacids, organic acid salts, and inorganic salts. Mixtures of the abovemembers are specifically contemplated as falling within the scope of theinvention. This member will typically be present in only a minor amount(e.g. less than about 20% by weight of the fluid).

The organic acid is typically a sulfonic acid or a carboxylic acid andthe anionic counter-ion of the organic acid salts are typicallysulfonates or carboxylates. Representative of such organic moleculesinclude various aromatic sulfonates and carboxylates such as p-toluenesulfonate, naphthalene sulfonate, chlorobenzoic acid, salicylic acid,phthalic acid and the like, where such counter-ions are water-soluble.Most preferred are salicylate, phthalate, p-toluene sulfonate,hydroxynaphthalene carboxylates, e.g. 5-hydroxy-1-naphthoic acid,6-hydroxy-1-naphthoic acid, 7-hydroxy-1-naphthoic acid,1-hydroxy-2-naphthoic acid, preferably 3-hydroxy-2-naphthoic acid,5-hydroxy-2-naphthoic acid, 7-hydroxy-2-naphthoic acid, and1,3-dihydroxy-2-naphthoic acid and 3,4-dichlorobenzoate. The organicacid or salt thereof typically aids the development of increasedviscosity which is characteristic of preferred fluids. Without wishingto be bound by any theory unless expressly noted otherwise in context,it is thought that association of the organic acid or salt thereof withthe micelle decreases the aggregation curvature of the micelle and thuspromotes the formation of a worm-like or rod-like micelle. The organicacid or salt thereof will typically be present in the viscoelastic fluidat a weight concentration of from about 0.1% to about 10%, moretypically from about 0.1% to about 7%, and even more typically fromabout 0.1% to about 6%.

The inorganic salts that are particularly suitable for use in theviscoelastic fluid include water-soluble potassium, sodium, and ammoniumsalts, such as potassium chloride and ammonium chloride. Additionally,calcium chloride, calcium bromide and zinc halide salts may also beused. The inorganic salts may aid in the development of increasedviscosity which is characteristic of preferred fluids. Further, theinorganic salt may assist in maintaining the stability of a geologicformation to which the fluid is exposed. Formation stability and inparticular clay stability (by inhibiting hydration of the clay) isachieved at a concentration level of a few percent by weight and as suchthe density of fluid is not significantly altered by the presence of theinorganic salt unless fluid density becomes an important consideration,at which point, heavier inorganic salts may be used. The inorganic saltwill typically be present in the viscoelastic fluid at a weightconcentration of from about 0.1% to about 30%, more typically from about0.1% to about 10%, and even more typically from about 0.1% to about 8%.Organic salts, e.g. trimethylammonium hydrochloride andtetramethylammonium chloride, may also be useful in addition to, or as areplacement for, the inorganic salts.

As an alternative to the organic salts and inorganic salts, or as apartial substitute therefor, one can use a medium to long chain alcohol(preferably an alkanol), preferably having five to ten carbon atoms, oran alcohol ethoxylate (preferably an alkanol ethoxylate) preferably of a12 to 16 carbon alcohol and having 1 to 6, preferably 1-4, oxyethyleneunits.

In the embodiment where the surfactant selected is an amine oxide, it ispreferably used in combination with an anionic surfactant containing ahydrophobe having at least about 14 carbon atoms. Examples of suitableanionic surfactants include alkyl sulfates or sulfonates having alkalimetal counter ions or alkyl carboxylates, wherein alkyl represents agroup that contains from about 14 to about 24 carbon atoms which may bebranched or straight chained and which may be saturated or unsaturated,and more preferably contains between about 16 and about 22 carbon atoms.

For this embodiment (amine oxide/anionic surfactant) the weight ratio ofthe amine oxide to anionic surfactant is from about 100:1 to about50:50.

In addition to the water-soluble salts and thickening agents describedhereinbefore, the viscoelastic fluid used as a hydraulic fracturingfluid may contain other conventional constituents which perform specificdesired functions, e.g., corrosion inhibitors, fluid-loss additives andthe like. A proppant can be suspended in the fracturing fluid. The pH ofthe fluid will typically range from strongly acidic (e.g. less than a pHof about 3) to slightly alkaline (e.g. from a pH just greater than 7.0to about 8.5, more typically to about 8.0) or moderately alkaline (e.g.a pH of about 8.5 to about 9.5). Strongly alkaline pHs (e.g. above a pHof about 10) should be avoided.

It is also conceivable to combine the above amphoteric/zwitterionicsurfactants with conventional anionic, nonionic and cationic surfactantsto get the desired viscoelastic fluid for a skilled worker. In typicalembodiments, the amphoteric/zwitterionic surfactant is typically presentin a major amount by weight of all surfactants, and more typically isessentially the only surfactant present. Typically, the viscoelasticfluid will be essentially free of anionic surfactants, e.g. it willcontain less than about 0.5%, more typically less than about 0.2%, evenmore typically less than 0.1% by weight of anionic surfactants.

To prepare the aqueous fluids in accordance with the present invention,the surfactant is added to an aqueous solution in which has beendissolved a water-soluble inorganic salt, e.g. potassium chloride orammonium chloride and/or at least one organic acid or water-solubleorganic acid salt to provide selective control of the loss of particlesuspension properties. In the embodiment wherein the fluid is a mixtureof water, and amine oxide surfactant and an anionic surfactant, a simplemixture of the three components is utilized. Standard mixing proceduresknown in the art can be employed since heating of the solution andspecial agitation conditions are normally not necessary. Of course, ifused under conditions of extreme cold such as found in Alaska, normalheating procedures should be employed. It has been found in someinstances preferable to dissolve the thickener into a lower molecularweight alcohol prior to mixing it with the aqueous solution. The lowermolecular weight alcohol, for instance isopropanol, functions as an aidto solubilize the thickener. Other similar agents may also be employed.Further, a defoaming agent such as a polyglycol may be employed toprevent undesirable foaming during the preparation of the viscoelasticfluid if a foam is not desirable under the conditions of the treatment.If a foam or gas-energized fluid is desired, any gas such as air,nitrogen, carbon dioxide and the like may be added.

The fluid of this invention is particularly useful in the handling ofparticles generated during the excavation of a geologic formation, e.g.digging, drilling, blasting, dredging, tunneling, and the like, forexample in the course of constructing roads, bridges, buildings, mines,tunnels and the like. The particles are mixed with the viscoelasticfluid by means which are effective to disperse the particles in thefluid. The particles generally have a particle size ranging from a finepowder to coarse gravel, e.g. dust, sand, and gravel. Particle sizeaffects the suspendability of excavation processing wastes. For example,small particles suspend better than large particles, and very fineparticles suspend so well that the mixture may become too thick totransport by pump or similar means. The distribution of excavationprocessing waste sizes is also important, as waste which containsparticles which span a wide range of sizes is more easily suspended thanwaste wherein the particles are of about the same size. Therefore, itmay be preferred to screen the waste particles prior to applying thepresent method to scalp off the particles that are too large to suspendto obtain a better particle size distribution.

The viscoelastic fluids of the present invention can be utilized tocarry earth or materials excavated during boring, excavating andtrenching operations in the deep foundation construction industry, thesubterranean construction industry and in tunneling, in well drillingand in other applications of earth support fluids. The ability of theexcavation tools or systems to hold and remove increased loading ofearth is improved by the suspending properties and lubricatingproperties of the surfactant viscoelastic fluids.

In one preferred embodiment of this invention, the surfactant can becombined with some fluid-loss control additives known in the industrylike water-soluble or water-dispersible polymers (guar and guarderivatives, xanthan, polyacrylamide, starch and starch derivatives,cellulosic derivatives, polyacrylates, polyDADMAC [poly(diallyl dimethylammonium chloride] and combinations thereof), clay (Bentonite andattapulgite) in order to give fluid-loss control properties to theexcavating fluid and contribute to the stabilization of the wall of theexcavation.

More comprehensive information can be found in The University ofHouston, Department of Chemical Engineering, Publication No UHCE 93-1entitled, Effect of Mineral and Polymer slurries on Perimeter LoadTransfer in Drilled shafts, published in January 1993, and PCT WO96/23849, the disclosures of which are incorporated by reference.

The above method for suspending solids has many applications,particularly in mining and the handling of mine tailings. The disclosureof U.S. Pat. No. 5,439,317 (Bishop et al.) is incorporated by referencein this regard. One application is to transport and place mineralprocessing waste in underground caverns or below grade cavities. Anotherapplication is for backfilling of open pits or quarries without the useof costly and labor intensive equipment for deployment. Additionally,the method can be used to place clay or other liners in holding orstorage ponds that are used to hold liquids and to prevent the entry ofthese liquids into the ground water regime and/or to place liners inlandfills for a similar purpose. Another application of the method, isfor the extinguishing and/or containment of coal mine fires by deployingquantities of solids below ground to seal the fire from sources ofoxygen. Still another application of the method is to place solids inpreviously mined cavities to prevent surface subsidence.

The hydraulic fracturing method of this invention uses otherwiseconventional techniques. The disclosure of U.S. Pat. No. 5,551,516(Norman et al.) is incorporated by reference in this regard. Oil-fieldapplications of various materials are described in “Oil-fieldApplications”, Encyclopedia of Polymer Science and Engineering, vol. 10,pp. 328-366 (John Wiley & Sons, Inc., New York, N.Y., 1987) andreferences cited therein, the disclosures of which are incorporatedherein by reference thereto.

Hydraulic fracturing is a term that has been applied to a variety ofmethods used to stimulate the production of fluids such as oil, naturalgas etc., from subterranean formations. In hydraulic fracturing, afracturing fluid is injected through a wellbore and against the face ofthe formation at a pressure and flow rate at least sufficient toovercome the overburden pressure and to initiate and/or extend afracture(s) into the formation. The fracturing fluid usually carries aproppant such as 20-40 mesh sand, bauxite, glass beads, etc., suspendedin the fracturing fluid and transported into a fracture. The proppantthen keeps the formation from closing back down upon itself when thepressure is released. The proppant filled fractures provide permeablechannels through which the formation fluids can flow to the wellbore andthereafter be withdrawn. Viscoelastic fluids have also been extensivelyused in gravel pack treatment.

In addition to the applications discussed above, the viscoelastic fluidsmay also be used as an industrial drift control agent, or as a rheologymodifier for personal care formulations (e.g. cleansers, conditioners,etc.) and household cleansers (e.g. detergent formulations). A detergentformulation of the viscoelastic fluids of this invention will furthercomprise a detersive surfactant. Examples of detersive surfactants andother conventional ingredients of detergent and/or personal careformulations are disclosed in U.S. Ser. No. 08/726,437, filed Oct. 4,1996, the disclosure of which is incorporated herein by reference.

Typically, the detersive surfactant will be anionic or nonionic.Preferred water-soluble anionic organic surfactants herein includelinear alkyl benzene sulfonates containing from about 10 to about 18carbon atoms in the alkyl group; branched alkyl benzene sulfonatescontaining from about 10 to about 18 carbon atoms in the alkyl group;the tallow range alkyl sulfates; the coconut range alkyl glycerylsulfonates; alkyl ether (ethoxylated) sulfates wherein the alkyl moietycontains from about 12 to 18 carbon atoms and wherein the average degreeof ethoxylation varies between 1 and 12, especially 3 to 9; the sulfatedcondensation products of tallow alcohol with from about 3 to 12,especially 6 to 9, moles of ethylene oxide; and olefin sulfonatescontaining from about 14 to 16 carbon atoms.

Specific preferred anionics for use herein include: the linear C₁₀-C₁₄alkyl benzene sulfonates (LAS); the branched C₁₀-C₁₄ alkyl benzenesulfonates (ABS); the tallow alkyl sulfates, the coconut alkyl glycerylether sulfonates; the sulfated condensation products of mixed C₁₀-C₁₈tallow alcohols with from about 1 to about 14 moles of ethylene oxide;and the mixtures of higher fatty acids containing from 10 to 18 carbonatoms.

Particularly preferred nonionic surfactants for use in liquid, powder,and gel applications include the condensation product of C₁₀ alcoholwith 3 moles of ethylene oxide; the condensation product of tallowalcohol with 9 moles of ethylene oxide; the condensation product ofcoconut alcohol with 5 moles of ethylene oxide; the condensation productof coconut alcohol with 6 moles of ethylene oxide; the condensationproduct of C₁₂ alcohol with 5 moles of ethylene oxide; the condensationproduct of C₁₂₋₁₃ alcohol with 6.5 moles of ethylene oxide, and the samecondensation product which is stripped so as to remove substantially alllower ethoxylate and non-ethoxylated fractions; the condensation productof C₁₂₋₁₃ alcohol with 2.3 moles of ethylene oxide, and the samecondensation product which is stripped so as to remove substantially alllower ethoxylated and non-ethoxylated fractions; the condensationproduct of C₁₂₋₁₃ alcohol with 9 moles of ethylene oxide; thecondensation product of C₁₄₋₁₅ alcohol with 2.25 moles of ethyleneoxide; the condensation product of C₁₄₋₁₅ alcohol with 4 moles ofethylene oxide; the condensation product of C₁₄₋₁₅ alcohol with 7 molesof ethylene oxide; and the condensation product of C₁₄₋₁₅ alcohol with 9moles of ethylene oxide.

Particular detersive applications for which the viscoelastic fluid willbe useful include as a thickener for acidic bathroom cleaners, such asthose disclosed in U.S. Pat. No. 5,639,722 (Kong et al.) and shower gelssuch as those disclosed in U.S. Pat. No. 5,607,678 (Moore et al.), thedisclosures of which are incorporated by reference. The viscoelasticfluids will also be useful in the manufacture of building products basedon plaster, plaster/lime, lime/cement or cement such as those disclosedin U.S. Pat. No. 5,470,383 (Schermann et al.) and foam fluids such asthose disclosed in U.S. Pat. No. 5,258,137 (Bonekamp et al.), thedisclosures of which are incorporated by reference. In particular, thefluid will be useful for improving the water retention of cementslurries and grouts allowing better pumpability and workability withminimal free water. The fluids will also be useful as thickeners foracidic (e.g. a pH of less than about 5) aqueous slurries of mineralcarbonates or oxides, e.g. iron oxide, cerium oxide, silica suspensions,titanium oxide, calcium carbonate, and zirconium oxide. In this regard,the disclosure of U.S. Pat. No. 4,741,781 (De Witte) is incorporated byreference.

The viscoelastic fluid of this invention will also be useful informulations for the agricultural delivery of solid fertilizers andpesticides such as micronutrients, biologicals, insecticides,herbicides, fungicides, and plant growth regulators. Such formulationsare typically aqueous suspensions or solutions comprised of a majoramount of water and an agriculturally effective amount of anagriculturally useful chemical. The viscoelastic fluid is typicallycombined with the other ingredients of the formulation in an amount thateffectively reduces the number of droplets below about 150 microns, i.e.the droplets most responsible for drift problems.

The following examples are presented to illustrate the preparation andproperties of aqueous viscoelastic surfactant based hydraulic fluids andshould not be construed to limit the scope of the invention, unlessotherwise expressly indicated in the appended claims. All percentages,concentrations, ratios, parts, etc. are by weight unless otherwise notedor apparent from the context of their use.

EXAMPLES Example 1

Viscoelastic surfactant solutions are prepared by adding 5 percent ofammonium chloride and 3 to 5 percent of dihydroxyethyl tallow glycinate(Mirataine TM®) to water. The systems were stirred until all of thesurfactant dissolved. All of the samples were observed to beviscoelastic by the bubble recoil test. Rheology of solution wasmeasured by Rheometric ARES at 25° C. The results are given below inTable 1.

TABLE 1 Shear rate Viscosity (cps) in 5% NH₄Cl (sec⁻¹) 3% Surfactant 4%Surfactant 5% Surfactant 10 1692.4 2619.8 3774.7 18 967.7 1490.6 2144 32555.5 851.6 1214.3 56 319.2 483.2 688.1 100 184.6 278 393.6 178 107.5159.3 225.4

Example 2

In a manner similar to Example 1, 0.3 percent of phthalic acid and 2 to4 percent of dihydroxyethyl tallow glycinate (Mirataine TM®) were putinto solution. All of the samples were observed to be viscoelastic bythe bubble recoil test. Rheological measurements were performed in themanner described in Example 1 at 25° C. The results are shown below inTable 2:

TABLE 2 Shear rate Viscosity (cps) in 0.3% phthalic acid (sec⁻¹) 2%Surfactant 3% Surfactant 4% Surfactant 10 791.5 1474.6 1968.7 18 455.3840.9 1101.5 32 262.4 490 564.5 56 152 279.2 361.7 100 88 160.9 356.6178 53 91.6 342.3

Example 3

The rheological measurements were also performed at higher temperaturesby FANN Rheometer. The results for 4 percent dihydroxyethyl tallowglycinate (Mirataine TM®) and 0.3 percent of phthalic acid solution areshown below in Table 3:

TABLE 3 Temperature (° F.) Viscosity at 100 rpm (cps) 82 170 129 51 18930 239 22 288 15

Example 4

The viscoelastic surfactant solutions are prepared by adding 5 percentof disodium tallowiminodipropionate (Mirataine T2C®) and 2.25 percent ofphthalic acid to water. The systems were stirred and warmed up to 50° C.until all of the phthalic acid dissolved. All of the samples wereobserved to be viscoelastic by the bubble recoil test. Rheology wasmeasured for viscosity and dynamic modulus G′(storage modulus) and G″(loss modulus) by a Rheometric SR-200 at 25° C. and 50° C. The resultsare shown in FIGS. 1 and 2.

Example 5

In a manner similar to Example 4, 5 percent of disodiumtallowiminodipropionate (Mirataine T2C®), 4 percent of NH₄Cl and1.75˜2.0 percent of phthalic acid in water were mixed together. All ofthe samples were observed to be viscoelastic by the bubble recoil test.Rheological measurements were performed in the manner described inExample 4 at 25° C. The results are shown in FIG. 3.

Example 6

The viscoelastic surfactant solutions are prepared by addition of 4˜5%percent of oleamidopropyl betaine (Mirataine BET-O®), 3% KCl and 0.5%phthalic acid to water. The system was stirred until all phthalic aciddissolved. Rheology was measured for steady viscosity and dynamicmodulus G′/G″ by Rheometric ARES at 25° C. The results are shown inFIGS. 4 and 5.

Example 7

A viscoelastic surfactant solution is prepared by mixing together in95.65 parts of water 4 parts of euricic amido propylene dimethyl amineoxide and 0.35 parts of sodium oleyl sulfate. The pH is adjusted to 8 bythe addition of NaOH. Its temperature stability is determined bymeasuring its viscosity in cps (at shear rate of 100 sec⁻¹). The resultsare shown in Table 4.

Example 8

A viscoelastic surfactant solution is prepared by mixing together in95.50 parts of water 4.0 parts of euricic amido propylene dimethyl amineoxide and 0.50 parts of sodium oleyl sulfate. Its temperature stabilityis determined by measuring its viscosity in cps(at shear rate of 100sec⁻¹). The results are shown in Table 4.

TABLE 4 Viscosity Viscosity Temperature (° F.) Example 8 Example 7 100282 247 120 302 293 140 308 305 160 168 237 180 162 166 200 230 231 220119 193 240 50 63 250 36 36 260 30 27 270 16 10

Example 9

A viscoelastic surfactant solution is prepared by mixing together in96.1 parts of water 3.0 parts of euricic amidopropyl amine oxide and 0.9parts of sodium behenyl sulfate. The pH is adjusted to 9 by the additionof NaOH. Its temperature stability is determined by measuring itsviscosity in cps (at shear rate of 100 sec⁻¹). The results are shown inTable 5.

Example 10

A viscoelastic surfactant solution is prepared by mixing together in94.8 parts of water 4.0 parts of euricic amidopropyl amine oxide and 1.2parts of sodium behenyl sulfate. The pH is adjusted to 9 by the additionof NaOH. Its temperature stability is determined by measuring itsviscosity in cps (at shear rate of 100 sec⁻¹). The results are shown inTable 5.

TABLE 5 Viscosity Viscosity Temperature (° F.) Example 9 Example 10 100175 234 120 168 226 140 169 297 160 256 518 180 309 454 200 276 173 220140 214 240 154 284 260 94 351 270 52 215 280 31 90 290 25 40 300 17 4

1-99. (canceled)
 100. A viscoelastic fluid, comprising: (1) an aqueousmedium; (2) erucyl amidopropyl betaine (3) a member selected from thegroup consisting of organic acids, organic acid salts, inorganic salts,and combinations of one or more organic acids or organic acid salts withone or more inorganic salts; wherein the fluid exhibits viscoelasticity.101. The fluid of claim 100, further comprising an anionic surfactant.102. The fluid of claim 101, wherein the anionic surfactant is presentat 1.2% or less by weight of the fluid.
 103. The fluid of claim 101,wherein the anionic surfactant is present at 0.9% or less by weight ofthe fluid.
 104. The fluid of claim 101, wherein the anionic surfactantis present at about 0.5% or less by weight of the fluid.
 105. The fluidof claim 100, wherein erucyl amidopropyl betaine is present at about 0.5wt % to about 10 wt % by weight of the fluid.
 106. The fluid of claim100, wherein erucyl amidopropyl betaine is present at about 0.5 wt % toabout 8 wt % by weight of the fluid.
 107. The fluid of claim 100,wherein erucyl amidopropyl betaine is present at about 0.5 wt % to about6 wt % by weight of the fluid.
 108. The fluid of claim 100, whereinerucyl amidopropyl betaine constitutes 89% or more by weight of allsurfactants present in the fluid.
 109. The fluid of claim 100, whereinerucyl amidopropyl betaine constitutes 92% or more by weight of allsurfactants present in the fluid.
 110. The fluid of claim 100, whereinthe member is an inorganic salt and is present at about 0.1% to about30% by weight.
 111. The fluid of claim 100, wherein the member is anorganic acid or salt thereof and is present at about 0.1% to about 10%by weight.
 112. The fluid of claim 100, further comprising a nonionicsurfactant or a cationic surfactant.
 113. The fluid of claim 100,further comprising an anionic surfactant, wherein the ratio of erucylamidopropyl betaine to anionic surfactant is 3⅓ to 1 or greater. 114.The fluid of claim 113, wherein the ratio of erucyl amidopropyl betaineto anionic surfactant is greater than 5 to
 1. 115. The fluid of claim114, wherein the ratio of erucyl amidopropyl betaine to anionicsurfactant is greater than 8 to
 1. 116. The fluid of claim 115, whereinthe ratio of erucyl amidopropyl betaine to anionic surfactant is greaterthan 12 to
 1. 117. The fluid of claim 100, further comprising an anionicsurfactant, wherein erucyl amidopropyl betaine is present at about 0.5wt % to about 10 wt % by weight of the fluid, wherein the ratio oferucyl amidopropyl betaine to anionic surfactant is 3⅓ to 1 or greater,wherein the member is an inorganic salt present at about 0.1% to about30% by weight or an organic acid or salt thereof present at about 0.1%to about 10% by weight.
 118. The fluid of claim 100, further comprisingan anionic surfactant, wherein erucyl amidopropyl betaine is present atabout 0.5 wt % to about 6 wt % by weight of the fluid, wherein the ratioof erucyl amidopropyl betaine to anionic surfactant is greater than 5 to1, wherein the member is an inorganic salt present at about 0.1% toabout 30% by weight or an organic acid or salt thereof present at about0.1% to about 10% by weight.
 119. (canceled)